JP3468925B2 - Waste incineration equipment - Google Patents

Waste incineration equipment

Info

Publication number
JP3468925B2
JP3468925B2 JP19757095A JP19757095A JP3468925B2 JP 3468925 B2 JP3468925 B2 JP 3468925B2 JP 19757095 A JP19757095 A JP 19757095A JP 19757095 A JP19757095 A JP 19757095A JP 3468925 B2 JP3468925 B2 JP 3468925B2
Authority
JP
Japan
Prior art keywords
combustion
air supply
gas
supply unit
grate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP19757095A
Other languages
Japanese (ja)
Other versions
JPH0942635A (en
Inventor
君代 徳田
利光 一ノ瀬
皓太郎 藤村
久夫 山本
正康 坂井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP19757095A priority Critical patent/JP3468925B2/en
Publication of JPH0942635A publication Critical patent/JPH0942635A/en
Application granted granted Critical
Publication of JP3468925B2 publication Critical patent/JP3468925B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、食堂,食品加工
業,漁港等の生ごみ、医療廃棄物,工場からの木材や廃
プラスチック等の廃棄物を焼却処理する装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for incinerating food waste, food waste, medical waste, wood, waste plastics and other wastes from factories, food processing industries, fishing ports and the like.

【0002】[0002]

【従来の技術】従来の技術を図2に基づいて説明する。2. Description of the Related Art A conventional technique will be described with reference to FIG.

【0003】焼却炉1の底部の火格子2の上に投入口3
より焼却物4を投入し、開閉蓋3aを閉じたあと、燃料
タンク7より送られたガス又は油燃料を燃料弁7aを通
して下部バーナ8aへ送り、下部空気口10aより取り込
まれた一次空気11aによって、火格子2の下面側(火格
子入口)で燃焼させて火炎12aをつくり、火格子上の焼
却物4を着火させこれを燃焼させる。
Inlet 3 on top of grate 2 at the bottom of incinerator 1.
After further incineration 4 and closing the opening / closing lid 3a, the gas or oil fuel sent from the fuel tank 7 is sent to the lower burner 8a through the fuel valve 7a, and by the primary air 11a taken in from the lower air port 10a. , The flame 12a is created by burning on the lower surface side (grate entrance) of the grate 2, and the incinerator 4 on the grate is ignited and burned.

【0004】焼却物4の下層は火格子2の下側から送ら
れる一次空気11aの酸素によって燃焼を起こし、燃焼層
4aをつくるが、酸素による燃焼を終えて、酸素が無く
なった燃焼ガスは上層の焼却物中の揮発分を気化させ揮
発層4bを形成する。揮発層4bを通過した燃焼ガス5
aは炭化水素,一酸化炭素のほかばいじん,臭素分等の
多量の可燃成分を含んでいる。
The lower layer of the incinerator 4 is combusted by the oxygen of the primary air 11a sent from the lower side of the grate 2 to form the combustion layer 4a, but the combustion gas depleted of oxygen after the combustion by oxygen is the upper layer. The volatile component in the incinerated substance is vaporized to form the volatile layer 4b. Combustion gas 5 that has passed through the volatile layer 4b
The a contains a large amount of combustible components such as hydrocarbons, carbon monoxide, dust and bromine.

【0005】従って、これを炉出口部に設けられた再燃
炉14aに導き、燃料弁7bを通して送られた燃料を上部
空気口10bより取り込まれた二次空気11bによって燃焼
させた火炎12bによって、燃焼ガス5a中に残存する可
燃成分を焼却し、清浄化された排ガス5bとして煙突1
6より大気へ排出するようになっている。
Therefore, this is guided to the reburning furnace 14a provided at the furnace outlet, and the fuel sent through the fuel valve 7b is burned by the flame 12b which is burned by the secondary air 11b taken in from the upper air port 10b. The combustible components remaining in the gas 5a are incinerated, and the chimney 1 is obtained as cleaned exhaust gas 5b.
It is designed to be discharged to the atmosphere from 6.

【0006】[0006]

【発明が解決しようとする課題】上記した従来のもの
は、近年普及した低公害形の焼却炉であって、低公害化
達成という点では所期の狙いに合致するものの、以下列
挙するような問題点を内在するものである。
The above-mentioned conventional one is a low-pollution type incinerator which has been popular in recent years, and it meets the intended purpose in terms of achieving low pollution, but is as follows. The problem is inherent.

【0007】(1)無煙・無臭の排ガス5bとするた
め、別個に独立した再燃炉を必要とし、設備が大形化
し、設備費が嵩む。
(1) Since the smokeless and odorless exhaust gas 5b is used, a separate and independent reburning furnace is required, and the equipment becomes large and the equipment cost increases.

【0008】(2)燃焼ガス5aの可燃成分量の変動が
激しいため再燃炉14aには着火・焼却を安定させるため
火炎12bを保持することが必要で、このために上部バー
ナ8bを設置し、バーナ用燃料を常時使用する必要があ
る。
(2) Since the amount of combustible components in the combustion gas 5a fluctuates significantly, it is necessary to hold the flame 12b in the reburning furnace 14a in order to stabilize ignition / incineration. For this purpose, the upper burner 8b is installed, It is necessary to constantly use burner fuel.

【0009】(3)焼却速度を上げるためには、下部バ
ーナ8aの燃料燃焼量を増やしたり、下部の一次空気11
aの吸い込み量を増やすことが必要であるが、焼却物4
の発熱量が高い廃プラスチック等の場合は、燃焼層4a
の温度が1300℃を越える高温になり、燃焼炉1をは
じめとする装置材料を焼損させ、装置寿命を著しく短命
化させる。
(3) In order to increase the incineration speed, the amount of fuel burned in the lower burner 8a is increased or the primary air 11 in the lower portion is heated.
It is necessary to increase the intake amount of a.
In the case of waste plastic with a high calorific value, the combustion layer 4a
Becomes higher than 1300 ° C., the material of the apparatus including the combustion furnace 1 is burnt out, and the life of the apparatus is remarkably shortened.

【0010】(4)焼却処理能力を上げるためには、焼
却物4を燃焼炉1内の燃焼速度に適合させて、連続もし
くは断続的に投入することが望ましいが、投入口3の開
閉蓋3aが開いているとき、ここから冷空気が入って燃
焼ガス5aを過冷却して、再燃炉14aの燃焼を妨げ、発
煙・臭気を排ガス5bが含んだまま排出されることがあ
る。
(4) In order to increase the incineration capacity, it is desirable to adapt the incineration material 4 to the combustion speed in the combustion furnace 1 and to continuously or intermittently charge it, but the opening / closing lid 3a of the charging port 3 is required. When is open, cold air may enter from here to supercool the combustion gas 5a, hinder combustion in the reburning furnace 14a, and emit smoke and odor while the exhaust gas 5b is still contained.

【0011】本発明は従来のものにおけるこれらの問題
点を解消し、新規にして有益な焼却装置を得ることを課
題とするものである。
An object of the present invention is to solve these problems in the prior art and to obtain a novel and useful incinerator.

【0012】[0012]

【課題を解決するための手段】従って本発明は、火格子
を備えた燃焼炉で、同燃焼炉上部の循環口から火格子下
部に燃焼ガスを循環させる循環通路を設け、同循環通路
内にはその始端側に循環する燃焼ガスの冷却装置を設け
ると共に末端側に一次空気と燃料を噴出させるバーナを
設け、上記火格子下部には循環燃焼ガス中の可燃成分を
燃焼させるガス燃室を形成し、同ガス燃室の後流には二
次空気供給部及び三次空気供給部と、上記循環燃焼ガス
の減温装置と、再燃室を設け、上記二次空気供給部は上
記再燃室の入口側に、上記三次空気供給部は同再燃室
に、上記減温装置は前記再燃室内で上記二次空気供給部
と三次空気供給部の中間に配置した廃棄物の焼却装置を
提供するものである。
SUMMARY OF THE INVENTION Therefore, the present invention is a combustion furnace having a grate, and a circulation passage for circulating combustion gas is provided from a circulation port in the upper portion of the combustion furnace to a lower portion of the grate. Is provided with a cooling device for the circulating combustion gas at its start end, a burner for ejecting primary air and fuel at the end, and a gas combustion chamber for burning combustible components in the circulating combustion gas under the grate. However, a secondary air supply unit and a tertiary air supply unit, a circulating combustion gas temperature reducing device, and a reburn chamber are provided in the downstream of the gas combustion chamber, and the secondary air supply unit is located above.
At the inlet side of the reburn chamber, the above-mentioned tertiary air supply unit is
In the reheating chamber, the temperature reducing device is provided with the secondary air supply unit.
And an incinerator for waste disposed between the secondary air supply section and the tertiary air supply section .

【0013】また、本発明は、火格子を備えた燃焼炉
で、同燃焼炉の焼却物投入部は開閉式扉と回転式投入器
兼用扉との二重構造とし、同燃焼炉上部の循環口から火
格子下部に燃焼ガスを循環させる循環通路を設け、同循
環通路内にはその始端側に循環する燃焼ガスの冷却装置
を設けると共に末端側でこの循環燃焼ガスの流れ方向と
略同一方向に一次空気と燃料を噴出させるバーナを設
け、上記火格子下部には循環燃焼ガス中の可燃成分を燃
焼させるガス燃室を形成し、同ガス燃室の後流には二次
空気供給部及び三次空気供給部と、上記循環燃焼ガスの
減温装置と、再燃室を設け、上記二次空気供給部は上記
再燃室の入口側に、上記三次空気供給部は同再燃室に、
上記減温装置は前記再燃室内で上記二次空気供給部と三
次空気供給部の中間に配置した廃棄物の焼却装置を提供
するものである。
Further, the present invention is a combustion furnace equipped with a grate, and the incinerator charging part of the combustion furnace has a double structure of an openable door and a door also serving as a rotary charging device, and the circulation at the upper part of the combustion furnace. A circulation passage for circulating the combustion gas from the mouth to the lower part of the grate is provided, and a cooling device for the combustion gas which circulates at the start end side is provided in the circulation passage, and the flow direction of the circulation combustion gas is substantially the same at the end side. A burner for injecting primary air and fuel is provided in the above, a gas combustion chamber for combusting combustible components in the circulating combustion gas is formed under the grate, and a secondary air supply unit and A tertiary air supply unit, a circulating combustion gas temperature reducing device, and a reburn chamber are provided, and the secondary air supply unit is
On the inlet side of the reburn chamber, the tertiary air supply unit is in the reburn chamber,
The temperature reducing device is connected to the secondary air supply unit and the third air supply unit in the reburn chamber.
It is intended to provide a waste incinerator arranged in the middle of the next air supply section .

【0014】即ち、本発明では、燃焼炉上部から火格子
下部を循環通路で連絡して同火格子下部にはガス燃室を
形成し、かつ、前記循環通路にはその始端側に燃焼ガ
スの冷却装置、末端側に一次空気を噴出するバーナを設
けると共に、火格子下部に設けたガス燃室の後流には二
次空気供給部及び三次空気供給部と循環燃焼ガスの減温
装置と再燃室を設け、かつ、上記二次空気供給部は上記
再燃室の入口側に、上記三次空気供給部は同再燃室に、
上記減温装置は前記再燃室内で上記二次空気供給部と三
次空気供給部の中間に配置し、各設置位置から一次、二
次、三次空気をそれぞれ分割して供給すると共に、冷却
装置及び減温装置で燃焼ガスの温度調整を図ることによ
り、燃焼ガス中の可燃成分を効果的に焼却し、また、焼
却物の種類により上記燃焼ガス中の可燃成分が多量にな
ったとしても再燃室で減温を考慮しつつ対処し、初期の
狙いを達成するものである。なお、更に加えて、上記燃
焼炉の焼却物投入部は開閉式扉と回転式投入器兼用扉と
の二重構造とし、また、上記循環通路内に設ける一次空
気と燃料を噴出させるバーナは、上記循環燃焼ガスの流
れ方向と略同一方向としたことにより、火格子の下部の
ガス燃室での燃焼は外部からの余剰空気の流入を防止
し、また循環燃焼ガスはエゼクタ効果により吸引されて
案内され、安定,迅速,かつ確実な燃焼の促進を図るも
のである。
[0014] That is, in the present invention, the combustion furnace to form a gas combustion chamber is from the top to the communication with the grate bottom grate bottom in a circular path, and the combustion gases to the starting end side of the circulation passage cooling device, distally provided with a burner for injecting primary air, and the reduced temperature device flow of the circulating combustion gases and the secondary air supply unit and the tertiary air supply unit after the gas combustion chamber is provided in the grate bottom A reburn chamber is provided, and the secondary air supply unit is
On the inlet side of the reburn chamber, the tertiary air supply unit is in the reburn chamber,
The temperature reducing device is connected to the secondary air supply unit and the third air supply unit in the reburn chamber.
It is placed in the middle of the secondary air supply unit, and primary, secondary, and tertiary air are separately supplied from each installation position , and the temperature of the combustion gas is adjusted by the cooling device and the temperature reducing device, so that the combustion gas Effectively incinerates the combustible components of the above, and even if the amount of combustible components in the combustion gas becomes large depending on the type of incinerated material, it is possible to take measures to reduce the temperature in the reburn chamber and achieve the initial aim. Is. In addition, in addition, the incinerator charging section of the combustion furnace has a double structure of an opening / closing door and a rotary charging / combining door, and a burner for ejecting primary air and fuel provided in the circulation passage is Combustion in the gas combustion chamber at the bottom of the grate prevents the inflow of excess air from the outside, and the circulation combustion gas is sucked by the ejector effect by setting the flow direction of the circulation combustion gas to be substantially the same. Guided to promote stable, quick, and reliable combustion.

【0015】[0015]

【発明の実施の形態】図1に基づき、本発明の実施の1
形態を説明する。なお、図中、上記した従来の技術と機
能的に対応する部分には同一符号を付すことにより本実
施の形態を一層理解し易いものとした。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiment 1 of the present invention will be described with reference to FIG.
The form will be described. In the drawings, the portions that functionally correspond to the above-described conventional technique are designated by the same reference numerals to make the present embodiment easier to understand.

【0016】燃焼炉1の下部には、火格子2を配設し、
上部には焼却物4の投入部が、開閉式扉3Aと回転式投
入器兼用扉3Bの二重構造となって、外部からの余剰空
気の流入を防ぎながら焼却物4を断続投入が出来るよう
になっている。
A grate 2 is arranged below the combustion furnace 1,
The injecting part 4 for the incineration product 4 has a double structure of an opening / closing door 3A and a rotary insertion device / door 3B so that the incineration product 4 can be intermittently injected while preventing the inflow of excess air from the outside. It has become.

【0017】火格子2上では、燃焼層4aとその上部に
揮発層4bをそれぞれ形成して燃焼が進行し、可燃成分
を含んだ燃焼ガス5Aが発生するが、この燃焼ガス5A
は循環口6aより循環通路6に導かれる。
On the grate 2, a combustion layer 4a and a volatile layer 4b are formed respectively on the combustion layer 4a and the combustion layer 4a, and the combustion proceeds to generate a combustion gas 5A containing a combustible component.
Is guided to the circulation passage 6 through the circulation port 6a.

【0018】なお、燃焼ガス5Aが高温化し温度調整の
必要ある場合には、必要水量を調整弁8Aで制御して減
温器7Aより噴霧する。
When the temperature of the combustion gas 5A rises and the temperature needs to be adjusted, the required amount of water is controlled by the adjusting valve 8A and sprayed from the temperature reducer 7A.

【0019】減温適性化した燃焼ガス5Aは燃料調整弁
12Aによって流量調整された燃料12と、空気弁10Aに
よって流量調整された一次空気11aでガス燃室14内に
形成された火炎13aに取り込まれて残存している燃焼
ガス5A中の可燃成分は燃焼消去される。
The combustion gas 5A whose temperature has been optimized is a fuel regulating valve.
The combustible components in the combustion gas 5A remaining after being taken into the flame 13a formed in the gas combustion chamber 14 by the fuel 12 whose flow rate is adjusted by 12A and the primary air 11a whose flow rate is adjusted by the air valve 10A are burned. Erased.

【0020】ここで、燃焼ガス5A,5Bの循環作動は
火炎13aを循環燃焼ガス5Cの流れ方向に噴出させる
ことによって、運動量相当の吸引効果(エゼクタ効果)
を発生させて行う。
Here, in the circulation operation of the combustion gases 5A and 5B, the flame 13a is ejected in the flow direction of the circulation combustion gas 5C, so that the suction effect (ejector effect) corresponding to the momentum is obtained.
Is generated.

【0021】火炎13aは略800から1300℃かつ
残酸素濃度が5%から16%となるように燃料12と一
次空気11aを燃料調整弁12Aと空気弁10Aによって流量
を調整し、最終的な燃焼排ガス5Eの清浄化と火格子上
の燃焼層4aの安定燃焼を図る。
In the flame 13a, the flow rates of the fuel 12 and the primary air 11a are adjusted by the fuel adjusting valve 12A and the air valve 10A so that the residual oxygen concentration is approximately 800 to 1300 ° C. and the residual oxygen concentration is 5% to 16%, and the final combustion is performed. The exhaust gas 5E is cleaned and the combustion layer 4a on the grate is stably burned.

【0022】また、焼却物4が廃プラスチックのような
高揮発分・高発熱量の場合は燃焼ガス5Aには多量の可
燃成分を含んでいるため、燃料12を遮断しても一次空
気量11aだけでは燃焼用空気が不足するため、ファン9
より送られる空気11の一部を二次空気11b,三次空気
11cに分割して供給し、上記ガス燃室14に続いて配置
した再燃室15で可燃成分の完全燃焼消去を図るように
なっている。
When the incinerated material 4 has a high volatile content and a high calorific value such as waste plastic, the combustion gas 5A contains a large amount of combustible components, and therefore the primary air amount 11a is maintained even if the fuel 12 is shut off. Because the combustion air is insufficient by itself, the fan 9
Part of the air 11 sent from the secondary air 11b, tertiary air
It is divided into 11c and supplied, and the reburning chamber 15 arranged subsequent to the gas combustion chamber 14 is designed to completely burn out combustible components.

【0023】ここの燃焼ガス5Dが高温となって器材焼
損の恐れがある場合は減温器7Bから噴霧水量を調整弁
8Dによって調節して供給し排ガス温度を調整する。さ
らに、ばいじん除去のためのセラミックスフォーム(多
気孔性のセラミックス板)集じん器17を煙突16の入
口部に設け、燃焼排ガス5Eの徹底浄化を図っている。
When the combustion gas 5D becomes high in temperature and there is a risk of burnout of equipment, the amount of water sprayed from the desuperheater 7B is adjusted by the adjusting valve 8D and supplied to adjust the exhaust gas temperature. Further, a ceramic foam (multi-porous ceramic plate) dust collector 17 for dust removal is provided at the inlet of the chimney 16 to thoroughly purify the combustion exhaust gas 5E.

【0024】なお、本実施の形態における燃焼に大きな
影響をおよぼす、空気の供給に関し説明を付加する。
A description will be added to the air supply which has a great influence on the combustion in the present embodiment.

【0025】焼却物4は火格子2の上で燃焼層4aとそ
の上部に揮発層4bを形成して燃焼炉1の内で燃焼し、
揮発層から発生した可燃成分を多量に含んだ燃焼ガス5
Aを発生するが、焼却物4の投入部が開閉式扉3A及び
回転式投入器兼用扉3Bによって、外部からの余剰空気
の流入を防いでいるため、循環通路6の系内に設けられ
たバーナ13の一次空気11a及び燃料12の噴出運動量
によって、燃焼ガス5Aがバーナ13に吸引され、可燃
成分を燃焼し消去することができる。
The incineration product 4 forms a combustion layer 4a on the grate 2 and a volatile layer 4b on the combustion layer 4a, and burns in the combustion furnace 1.
Combustion gas containing a large amount of combustible components generated from the volatile layer 5
A is generated, but the injecting part of the incineration material 4 is provided in the system of the circulation passage 6 because the opening / closing door 3A and the rotary type injector / combined door 3B prevent the inflow of excess air from the outside. The combustion gas 5A is sucked into the burner 13 due to the ejection momentum of the primary air 11a and the fuel 12 of the burner 13, and the combustible components can be burned and eliminated.

【0026】この燃焼ガス5Cの一部は火格子2を通っ
て燃焼炉1へ入り、加熱された燃焼用空気(酸素濃度は
外気より低い)として有効燃焼に与り、焼却速度を加速
し、短時間で焼却を完了させる。
A part of the combustion gas 5C enters the combustion furnace 1 through the grate 2 and is effectively burned as heated combustion air (oxygen concentration is lower than the outside air) to accelerate the incineration rate, Complete incineration in a short time.

【0027】このように投入部3の開閉が二重構造とな
っていることから、外部空気の流入を遮断しながら、断
続的に焼却物4を投入できるため、小形で大容量の焼却
能力を持たせることができる。
Since the opening / closing of the charging unit 3 has a double structure as described above, the incinerator 4 can be intermittently charged while blocking the inflow of external air, so that the incineration capacity of a small and large capacity can be obtained. You can have it.

【0028】また、廃プラスチック等の高揮発分・高発
熱量の焼却物4の場合は、燃焼ガス5Aに多量の可燃成
分をもつことになるが、これをバーナ13で燃焼させる
と1300℃を越える高温ガスを発生させるため、減温
器7A及び7Bと燃焼用空気の分割された一次空気11
a,二次空気11b,三次空気11cの供給によって、器材
の焼損を防いでいる。
Further, in the case of the incinerated matter 4 having a high volatile content and a high calorific value such as waste plastic, the combustion gas 5A has a large amount of combustible components, but when burned by the burner 13, 1300 ° C. In order to generate high-temperature gas that exceeds, the primary air divided by the desuperheaters 7A and 7B and combustion air 11
By supplying a, secondary air 11b, and tertiary air 11c, burnout of the equipment is prevented.

【0029】このように本実施の形態によれば、焼却物
4の投入部で開閉式扉3Aと回転式投入器兼用扉3Bの
二重構造により外部からの余剰空気の流入を防ぎつつ断
続的に焼却物4を投入できるようにし、燃焼ガス5Aを
循環通路6を通して、火格子2の下側に設けたガス燃室
14へ、一次空気11aと燃料12の噴射による流体の運
動量による吸引効果によって導き、これらによりバーナ
13の火炎13aによって燃焼ガス5a中に含まれる可燃
成分を燃焼消去することができる。
As described above, according to the present embodiment, the double structure of the openable door 3A and the rotary door 3B serving as the rotary inserter at the input portion of the incineration material 4 is intermittent while preventing the inflow of excess air from the outside. The incinerated matter 4 can be charged into the gas combustion chamber 5 through the circulation passage 6 into the gas combustion chamber 14 provided below the grate 2 by the suction effect of the momentum of the fluid by the injection of the primary air 11a and the fuel 12. The burnable components contained in the combustion gas 5a can be burned out by the flame 13a of the burner 13 by these guides.

【0030】さらに、ガス燃室14で発生した高温ガス
の一部が火格子2を通って燃焼炉1の内の燃焼に与るた
め、燃焼層4aの安定したかつ速度の速い燃焼が可能と
なる。
Further, since a part of the high temperature gas generated in the gas combustion chamber 14 passes through the grate 2 and contributes to the combustion in the combustion furnace 1, the combustion layer 4a can be stably and rapidly burned. Become.

【0031】また、ガス燃室14も火格子2の下面から
の熱ふく射を受け、安定した火炎13aを形成できるの
で、燃焼ガス5Aの可燃成分の発熱量が多い場合には燃
料12の供給を止め燃料費を節減することも可能であ
る。
Further, since the gas combustion chamber 14 can also receive the heat radiation from the lower surface of the grate 2 and form a stable flame 13a, the fuel 12 should be supplied when the calorific value of the combustible component of the combustion gas 5A is large. It is also possible to save fuel cost for stop.

【0032】さらに、廃プラスチックのような高揮発分
・高発熱量の焼却物の場合でも、減温器7A及び7Bと
二次・三次空気11b及び11cを制御することによって、
器材の焼損を抑えながら発煙・臭気を出すことのない、
浄化排ガスの焼却処理が可能となる。
Further, even in the case of incinerated materials with high volatile content and high calorific value such as waste plastic, by controlling the desuperheaters 7A and 7B and the secondary and tertiary air 11b and 11c,
Does not emit smoke or odor while suppressing burnout of equipment,
It becomes possible to incinerate the purified exhaust gas.

【0033】すなわち、各種性状の焼却物4を無煙・無
臭に近い焼却処理することができ、外部からの燃料使用
量を最小限にし、かつ、燃焼炉内の燃焼速度を高め、燃
焼速度に適合した焼却物の投入が可能なことから、高効
率・経済的な低公害形の焼却装置となる。
That is, the incinerator 4 of various properties can be incinerated almost smokelessly and odorlessly, the amount of fuel used from the outside can be minimized, and the combustion rate in the combustion furnace can be increased to meet the combustion rate. Since it is possible to put incinerated waste, it is a highly efficient and economical low pollution type incinerator.

【0034】以上、本発明を図示の実施の形態について
説明したが、本発明はかかる実施の形態に限定されず、
本発明の範囲内でその具体的構造に種々の変更を加えて
よいことはいうまでもない。
Although the present invention has been described with reference to the illustrated embodiments, the present invention is not limited to such embodiments.
It goes without saying that various modifications may be made to the specific structure within the scope of the present invention.

【0035】[0035]

【発明の効果】以上説明したように本発明によれば、燃
焼ガスの循環通路にはその始端側に冷却装置を設ける
と共に末端側に一次空気と燃料とを噴出するバーナを設
け、かつ、火格子下部に設けたガス燃室の後流には二次
空気供給部及び三次空気供給部と循環燃焼ガスの減温装
置、そして再燃室を設け、かつ、上記二次空気供給部は
上記再燃室の入口側に、上記三次空気供給部は同再燃室
に、上記減温装置は前記再燃室内で上記二次空気供給部
と三次空気供給部の中間に配置する等の工夫により、一
次、二次、三次空気をそれぞれ分割して供給すると共
に、冷却装置及び減温装置で燃焼ガスの温度調整を図
り、循環通路内を流れる燃焼ガス中の可燃成分を燃焼消
去し併せて火格子を介して燃焼炉内の燃焼を、安定,迅
速,かつ確実に促進し、また、焼却物の種類により上記
燃焼ガス中の可燃成分が多量になったとしても再燃室で
減温を考慮しつつ対処し、以て発煙,臭気を出すことな
く浄化排ガスの焼却処理が可能となり、高効率,経済的
な低公害形の焼却装置を得ることができたものである。
According to the present invention as described in the foregoing, it is in the circulation passage of combustion gas provided burner for injecting the primary air and fuel to the terminal provided with a cooling device for the starting side, and, A secondary air supply unit, a tertiary air supply unit, a temperature reducing device for circulating combustion gas, and a reburn chamber are provided in the wake of the gas combustion chamber provided under the grate , and the secondary air supply unit is
On the inlet side of the reburn chamber, the tertiary air supply unit is located in the reburn chamber.
In the reheating chamber, the temperature reducing device is provided with the secondary air supply unit.
If by devising such disposed intermediate tertiary air supply, primary, secondary, and tertiary air is supplied by dividing each work to temperature adjustment of the combustion gases in the cooling device and temperature reducing device, the circulation passage The combustible components in the combustion gas flowing through the combustion chamber are burned out, and the combustion in the combustion furnace is promoted in a stable, quick, and reliable manner through the grate, and the combustible components in the combustion gas depend on the type of incineration material. Even if there is a large amount of waste gas, it will be possible to deal with it by taking into account the temperature decrease in the reburn chamber, and it will be possible to incinerate the purified exhaust gas without producing smoke or odor, and a highly efficient and economical low pollution type incinerator can be installed. I was able to get it.

【0036】また、請求項2の発明によれば、上記請求
項1の発明の構成に加えて上記燃焼炉の焼却物投入部は
開閉式扉と回転式投入器兼用扉との二重構造とし、ま
た、上記循環通路内に設ける一次空気と燃料を噴出させ
るバーナは、上記循環燃焼ガスの流れ方向と略同一方向
としたことにより、火格子の下部のガス燃室での燃焼
は、外部からの余剰空気の流入防止、循環通路の冷却効
果、エゼクタ効果、更にはガス燃室内の熱ふく射等との
諸効果が相俟って、循環通路内を流れる燃焼ガス中の可
燃成分を燃焼消去し併せて火格子を介して燃焼炉内の燃
焼を、安定,迅速,かつ確実に促進し、高効率,経済的
な低公害形の焼却装置を得ることのできたものである。
According to the invention of claim 2, the above-mentioned claim
In addition to the constitution of the invention of Item 1, the incinerator input section of the combustion furnace is
It has a double structure with a door that can be opened and closed and a door that also serves as a rotary type feeder.
In addition, the primary air and fuel provided in the circulation passage are jetted out.
The burner is in the same direction as the flow direction of the circulating combustion gas.
And the combustion in the gas combustion chamber below the grate
Prevents the inflow of excess air from the outside and the cooling effect of the circulation passage.
With the result, the ejector effect, the heat radiation in the gas combustion chamber, etc.
Due to the combined effects, there is a possibility that the combustion gas flowing in the circulation passage
Combustion components in the combustion furnace are burned out through the grate.
It was possible to obtain a highly efficient and economical low-pollution incinerator that promotes burning in a stable, quick, and reliable manner.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の実施の1形態を示す説明図。FIG. 1 is an explanatory diagram showing an embodiment of the present invention.

【図2】従来のものを示す説明図。FIG. 2 is an explanatory view showing a conventional one.

【符号の説明】[Explanation of symbols]

1 燃焼炉 2 火格子 3A 開閉式扉 3B 回転式投入器兼用扉 4 焼却物 4a 燃焼層 4b 揮発層 6 循環通路 7A 冷却装置 7B 減温装置 11 空気 11a 一次空気 11b 二次空気 11c 三次空気 13 バーナ 14 ガス燃室 15 再燃室 1 combustion furnace 2 grate 3A openable door 3B Revolving type inserter combined door 4 Incinerated matter 4a Combustion layer 4b Volatile layer 6 circulation passages 7A cooling device 7B temperature reducer 11 air 11a Primary air 11b Secondary air 11c Tertiary air 13 burners 14 gas combustion chamber 15 Reburn room

───────────────────────────────────────────────────── フロントページの続き (72)発明者 山本 久夫 長崎市深堀町5丁目717番地1 長菱エ ンジニアリング株式会社内 (72)発明者 坂井 正康 長崎市深堀町5丁目717番地1 長菱エ ンジニアリング株式会社内 (56)参考文献 特開 平5−26422(JP,A) 実開 昭55−150232(JP,U) 特公 昭51−30397(JP,B1) (58)調査した分野(Int.Cl.7,DB名) F23G 5/00 119 F23G 5/027 F23G 5/14 - 5/16 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Hisao Yamamoto, 5-1,717, Fukahori-cho, Nagasaki-shi, Naganami Engineering Co., Ltd. (72) Masayasu Sakai 5-717, Fukahori-cho, Nagasaki-shi 1 Nagahishi (56) References Japanese Unexamined Patent Publication No. 5-26422 (JP, A) Actual Development 55-150232 (JP, U) JP-B 51-30397 (JP, B1) (58) Fields investigated ( Int.Cl. 7 , DB name) F23G 5/00 119 F23G 5/027 F23G 5/14-5/16

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 火格子を備えた燃焼炉で、同燃焼炉上部
の循環口から火格子下部に燃焼ガスを循環させる循環通
路を設け、同循環通路内にはその始端側に循環する燃焼
ガスの冷却装置を設けると共に末端側に一次空気と燃料
を噴出させるバーナを設け、上記火格子下部には循環燃
焼ガス中の可燃成分を燃焼させるガス燃室を形成し、同
ガス燃室の後流には二次空気供給部及び三次空気供給部
と、上記循環燃焼ガスの減温装置と、再燃室を設け、上
記二次空気供給部は上記再燃室の入口側に、上記三次空
気供給部は同再燃室に、上記減温装置は前記再燃室内で
上記二次空気供給部と三次空気供給部の中間に配置した
ことを特徴とする廃棄物の焼却装置。
1. A combustion furnace having a grate, wherein a circulation passage for circulating a combustion gas from a circulation port at an upper portion of the combustion furnace to a lower portion of the grate is provided, and a combustion gas circulating at a starting end side of the circulation passage. A burner for ejecting primary air and fuel is provided at the end side of the cooling device, and a gas combustion chamber for combustible components in the circulating combustion gas is formed under the grate. a secondary air supply unit and the tertiary air supply unit, a temperature decreasing device of the circulating combustion gas, the relapse chamber provided in the upper
The secondary air supply unit is located on the inlet side of the reburn chamber, and the tertiary air
The air supply unit is in the reburn chamber, and the temperature reducing device is in the reburn chamber.
A waste incinerator, which is arranged between the secondary air supply section and the tertiary air supply section .
【請求項2】 火格子を備えた燃焼炉で、同燃焼炉の焼
却物投入部は開閉式扉と回転式投入器兼用扉との二重構
造とし、同燃焼炉上部の循環口から火格子下部に燃焼ガ
スを循環させる循環通路を設け、同循環通路内にはその
始端側に循環する燃焼ガスの冷却装置を設けると共に
端側でこの循環燃焼ガスの流れ方向と略同一方向に一次
空気と燃料を噴出させるバーナを設け、上記火格子下部
には循環燃焼ガス中の可燃成分を燃焼させるガス燃室を
形成し、同ガス燃室の後流には二次空気供給部及び三次
空気供給部と、上記循環燃焼ガスの減温装置と、再燃室
設け、上記二次空気供給部は上記再燃室の入口側に、
上記三次空気供給部は同再燃室に、上記減温装置は前記
再燃室内で上記二次空気供給部と三次空気供給部の中間
配置したことを特徴とする廃棄物の焼却装置。
2. A combustion furnace equipped with a grate, wherein the incinerator charging part of the combustion furnace has a double structure of an openable door and a door also serving as a rotary charging device, and the grate is introduced from the circulation port at the upper part of the combustion furnace. the circulation path for circulating the combustion gas in the lower provided the in the circulation passage that
Install a cooling device for the combustion gas that circulates at the start end and
A burner for ejecting primary air and fuel is provided on the end side in a direction substantially the same as the flow direction of the circulating combustion gas, and a gas combustion chamber for combustible components in the circulating combustion gas is formed under the grate. A secondary air supply unit and a tertiary air supply unit, a temperature reducing device for the circulating combustion gas, and a reburn chamber are provided in the wake of the gas combustion chamber, and the secondary air supply unit is provided on the inlet side of the reburn chamber.
The tertiary air supply unit is in the reburn chamber, the temperature reducing device is
Between the secondary air supply section and the tertiary air supply section in the reburn chamber
A waste incinerator characterized by being placed in.
JP19757095A 1995-08-02 1995-08-02 Waste incineration equipment Expired - Fee Related JP3468925B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19757095A JP3468925B2 (en) 1995-08-02 1995-08-02 Waste incineration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19757095A JP3468925B2 (en) 1995-08-02 1995-08-02 Waste incineration equipment

Publications (2)

Publication Number Publication Date
JPH0942635A JPH0942635A (en) 1997-02-14
JP3468925B2 true JP3468925B2 (en) 2003-11-25

Family

ID=16376705

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3468925B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2000273193A1 (en) * 2000-09-21 2002-04-02 S.Mac Co., Ltd. Incinerator
JP2008190808A (en) * 2007-02-06 2008-08-21 Soai:Kk Combustion device
CN102242935A (en) * 2010-05-11 2011-11-16 吴学良 Novel garbage and biomass fuel combustion furnace and combustion method
KR101513877B1 (en) * 2014-05-14 2015-04-23 에스지티(주) Refuse Plastic Fuel Incinerator
CN104100980B (en) * 2014-07-01 2016-03-16 深圳合续环境科技有限公司 A kind of small-sized rubbish charing combustion furnace

Also Published As

Publication number Publication date
JPH0942635A (en) 1997-02-14

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